Methods for producing diesel range materials having improved cold flow properties

Abstract

Embodiments of a method for producing a diesel range material having improved cold flow properties are provided. In one embodiment, the method includes the steps of providing a waxy diesel range feedstock, producing an intermediary product stream containing a predetermined amount of oxygenated organocompounds from the waxy diesel range feedstock, and contacting the intermediary product stream with a dewaxing catalyst under process conditions at which the oxygenated organocompounds chemically interact with the dewaxing catalyst to convert a portion of the n-paraffins within the intermediary product stream to iso-paraffins while minimizing cracking of the diesel range material.

1 . A method for producing a diesel range material having improved cold flow properties, the method comprising the steps of:
 providing a waxy diesel range feedstock;   producing an intermediary product stream containing a predetermined amount of oxygenated organocompounds from the waxy diesel range feedstock; and   contacting the intermediary product stream with a dewaxing catalyst under process conditions at which the oxygenated organocompounds chemically interact with the dewaxing catalyst to convert a portion of the n-paraffins within the intermediary product stream to iso-paraffins while minimizing cracking of the diesel range material.   
     
     
         2 . A method according to  claim 1  wherein the step of providing a waxy diesel range feedstock comprises supplying a waxy diesel range feedstock containing n-paraffins and oxygenated organocompounds, and wherein the step of producing an intermediary product stream comprises removing a portion of the oxygenated organocompounds from the waxy diesel range feedstock while retaining a predetermined amount of oxygenated organocompounds therein. 
     
     
         3 . A method according to  claim 2  wherein the predetermined amount of oxygenated organocompounds retained within the waxy diesel range feedstock comprises about 200 to about 2000 parts per million by weight oxygen. 
     
     
         4 . A method according to  claim 2  wherein the step of supplying a waxy diesel range feedstock comprises deriving the waxy diesel range feedstock from a biorenewable source. 
     
     
         5 . A method according to  claim 4  wherein the step of deriving the waxy diesel range feedstock from a biorenewable source comprises deriving the waxy diesel range feedstock from a vegetable oil. 
     
     
         6 . A method according to  claim 4  wherein the step of deriving the waxy diesel range feedstock from a biorenewable source comprises deriving the waxy diesel range feedstock from algae. 
     
     
         7 . A method according to  claim 4  wherein the step of deriving the waxy diesel range feedstock from a biorenewable source comprises deriving the waxy diesel range feedstock from an animal-based source. 
     
     
         8 . A method according to  claim 2  wherein the step of supplying a waxy diesel range feedstock comprises producing the waxy diesel range feedstock from carbon monoxide and hydrogen utilizing Fischer-Tropsch synthesis. 
     
     
         9 . A method according to  claim 2  wherein step of contacting the intermediary product stream with a dewaxing catalyst comprises hydroisomerizing the intermediary product stream at temperatures between about 400° Fahrenheit (about 204° Celsius) and about 750° Fahrenheit (about 399° Celsius). 
     
     
         10 . A method according to  claim 2  wherein step of contacting the intermediary product stream with a dewaxing catalyst comprises hydroisomerizing the intermediary product stream at temperatures between about 550° Fahrenheit (about 288° Celsius) and about 600° Fahrenheit (about 316° Celsius). 
     
     
         11 . A method according to  claim 2  wherein step of contacting the intermediary product stream with a dewaxing catalyst comprises hydroisomerizing the intermediary product stream under pressures between about 200 pounds per square inch gauge (about 1379 kilopascal) and about 1500 pounds per square inch gauge (about 10,342 kilopascal). 
     
     
         12 . A method according to  claim 2  wherein step of contacting the intermediary product stream with a dewaxing catalyst comprises hydroisomerizing the intermediary product stream under pressures between about 500 pounds per square inch gauge (about 3447 kilopascal) and about 800 pounds per square inch gauge (5516 kilopascal). 
     
     
         13 . A method according to  claim 2  wherein step of contacting the intermediary product stream with a dewaxing catalyst comprises hydroisomerizing the intermediary product stream while adding hydrogen at a rate of about 500 to about 10,000 Standard Cubic Feet per Barrel (about 84.26 to about 1685 Normal Cubic Meters per Cubic Meter). 
     
     
         14 . A method according to  claim 2  wherein step of contacting the intermediary product stream with a dewaxing catalyst comprises hydroisomerizing the intermediary product stream while adding hydrogen at a rate of about 2,500 to about 5,000 Standard Cubic Feet per Barrel (about 421.3 to about 842.6 Normal Cubic Meters per Cubic Meter). 
     
     
         15 . A method according to  claim 1  wherein the oxygenated organocompounds comprise at least one of the group consisting of organic acids and alcohols. 
     
     
         16 . A method according to  claim 15  wherein the oxygenated organocompounds comprise carboxylic acid. 
     
     
         17 . A method according to  claim 1  wherein the step of providing a waxy diesel range feedstock comprises deriving the waxy diesel range feedstock from a petroleum-based source, and wherein the step of producing an intermediary product stream comprises:
 hydrotreating the waxy diesel range feedstock; and 
 after hydrotreating, adding a predetermined quantity of oxygenated organocompounds to the waxy diesel range feedstock. 
 
     
     
         18 . A method for producing a diesel range material having improved cold flow properties, the method comprising the steps of:
 deriving a diesel range feedstock containing n-paraffins and oxygenated organocompounds from a biorenewable source;   removing a portion of the oxygenated organocompounds to yield an intermediary product stream containing a predetermined amount of retained oxygenated organocompounds; and   hydroisomerizing the intermediary product stream with a dewaxing catalyst under process conditions at which the oxygenated organocompounds chemically interact with the dewaxing catalyst to increase catalyst selectivity and provide a diesel range material having an improved iso-normal paraffin ratio.   
     
     
         19 . A method according to  claim 18  wherein the step of hydroisomerizing the intermediary product stream comprises contacting the intermediary product stream with the dewaxing catalyst at temperatures between about 550° Fahrenheit (about 288° Celsius) and about 600° Fahrenheit (about 316° Celsius), under pressures between about 500 pounds per square inch gauge (about 3447 kilopascal) and about 800 pounds per square inch gauge (5516 kilopascal), and at hydrogen addition rates of about 2,500 to about 5,000 Standard Cubic Feet per Barrel (about 421.3 to about 842.6 Normal Cubic Meters per Cubic Meter). 
     
     
         20 . A method for producing a diesel range material having improved cold flow properties, the method comprising the steps of:
 converting carbon monoxide and hydrogen into the waxy diesel range feedstock utilizing Fischer-Tropsch synthesis;   removing a portion of the oxygenated organocompounds to yield a intermediary product stream containing a predetermined amount of retained oxygenated organocompounds; and   hydroisomerizing the intermediary product stream with a dewaxing catalyst under process conditions at which the oxygenated organocompounds chemically interact with the dewaxing catalyst to increase catalyst selectivity and provide a diesel range material having an improved iso-normal paraffin ratio.